Dynamic modelling, transient behaviour analysis and scheduling of volatile organic compound (VOC) abatement systems for the pharma industry
dc.contributor.advisor
Gerogiorgis, Dimitrios
dc.contributor.advisor
Koutsos, Vasileios
dc.contributor.advisor
Polydorides, Nick
dc.contributor.author
Tzanakopoulou, Vasiliki
dc.contributor.sponsor
Scottish Research Partnership in Engineering (SRPe)
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dc.contributor.sponsor
GlaxoSmithKline
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dc.contributor.sponsor
University of Edinburgh
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dc.date.accessioned
2024-11-14T11:54:17Z
dc.date.available
2024-11-14T11:54:17Z
dc.date.issued
2024-11-14
dc.description.abstract
Active Pharmaceutical Ingredient (API) manufacturing is heavily reliant on solvents for
reactions and separations. Among them, Volatile Organic Compounds (VOCs) reign supreme,
although their emissions pose a risk both to the environment and human health. With the effects
of climate change becoming more prominent, stringent regulations are in place to ensure the
enforcement of environment-conscious industrial. Adsorption on activated carbon beds is an
established VOC control technology, often preferred on an industrial level due to the low cost
of installation and maintenance, as well as its effectiveness in treating large volumetric streams
containing trace amounts of pollutants. However, the simultaneous feeding of varying
composition and load waste streams from plant-wide process vents under batch operation
causes quick and irregular bed saturation, leading to sub-optimal process efficiency, with
higher operational costs due to frequent adsorbent material regeneration outsourcing. Despite
the multitude of studies on adsorption over the years, there is a profound mismatch towards the
proportion of research focused on multicomponent VOC adsorption under realistic industrial
conditions. Mathematical modelling and simulations are valuable tools towards understanding
the complex interactions of competing solvent emission streams and allow process
optimisation without the need for costly and resource-intensive pilot plant experiments.
This PhD thesis aims to elucidate the intrinsic relationships between complex pharmaceutical
manufacturing solvent vapour mixtures and propose operational optimisation scenarios to
minimise environmental leak risks as well as maximise process efficiency, at an even lower
operational cost. In order to address the dire need for reliable thermodynamic parameter values,
a Langmuir Isotherm parameter database is established for organic solvents based on published
experimental data. Next, a dynamic, multicomponent, nonisothermal adsorption model is
constructed and used to highlight the interactions of key VOC binary mixtures under a range
of steady-state and transient feed conditions, temperatures, activated carbon bed structures,
column lengths and stream velocities. Furthermore, Hodograph Theory breakthrough metrics
are compared with validated simulation results to test the extrapolation potential of single
component mixture predictions to multicomponent mixtures as a quick, operational plant
decision-making tool. The dynamic model simulation results for the different mixtures are then
employed to inform Mixed Integer Linear Programming (MILP) scheduling models for process
optimisation and comparative economic evaluation. This PhD thesis highlights the immense
value of systematic and rigorous model-based simulation and optimisation campaigns for VOC
emission abatement systems in the pharmaceutical industry.
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dc.identifier.uri
https://hdl.handle.net/1842/42650
dc.identifier.uri
http://dx.doi.org/10.7488/era/5344
dc.language.iso
en
en
dc.publisher
The University of Edinburgh
en
dc.relation.hasversion
Tzanakopoulou, V. C., A.; Castro-Rodriguez, D.; Gerogiorgis, D.I. (2022). Multicomponent, nonisothermal voc adsorption modelling for pharmaceutical effluent purification: Effect of operating conditions on bed performance. Computer Aided Chemical Engineering, 51, 331-336
en
dc.relation.hasversion
Tzanakopoulou, V. E., Pollitt, M., Castro-Rodriguez, D., Costa, A., & Gerogiorgis, D. I. (2023). Dynamic modelling, simulation and theoretical performance analysis of volatile organic compound (voc) abatement systems in the pharma industry. Computers & Chemical Engineering, 174
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dc.subject
Dynamic modelling
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dc.subject
transient behaviour analysis
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dc.subject
volatile organic compound (VOC) abatement systems
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dc.subject
Active Pharmaceutical Ingredient
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dc.subject
Hodograph Theory
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dc.subject
Mixed Integer Linear Programming
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dc.title
Dynamic modelling, transient behaviour analysis and scheduling of volatile organic compound (VOC) abatement systems for the pharma industry
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dc.type
Thesis or Dissertation
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dc.type.qualificationlevel
Doctoral
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dc.type.qualificationname
PhD Doctor of Philosophy
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